System for producing cryogenic liquefied industrial gas

• US 5,799,505 A
• Filed: 07/28/1997
• Issued: 09/01/1998
• Est. Priority Date: 07/28/1997
• Status: Expired due to Term

• Current Assignee: Praxair Technology Incorporated (Linde Plc)
• Original Assignee: Praxair Technology Incorporated (Linde Plc)
• Inventors: Cribbin, Nancy Rose, Bonaquist, Dante Patrick, Billingham, John Fredric, Weber, Joseph Alfred, Nenov, Neno Todorov
• Primary Examiner(s): Capossela, Ronald C.
• Application Number:
  US08/901,350
• Time in Patent Office: 400 Days
• Field of Search: 62/613, 62/619, 62/908, 62/615
• US Class Current: 62/613
• CPC Class Codes: F25J 1/0015 Nitrogen
• CPC Class Codes: F25J 1/0017 Oxygen
• CPC Class Codes: F25J 1/0037 of a return stream
• CPC Class Codes: F25J 1/004 by flash gas recovery F25J1/0267 takes precedence
• CPC Class Codes: F25J 1/0202 in a quasi-closed internal refrigeration loop F25J1/0208, F25J1/0219, F25J1/0224 take precedence
• CPC Class Codes: F25J 1/0228 Coupling of the liquefaction unit to other units or processes, so-called integrated processes combined plants, e.g. engine plant combined with an industrial process F01K23/064; gas turbine plants in combination with other processes F02C6/00
• CPC Class Codes: F25J 1/0232 integration within a pressure letdown station of a high pressure pipeline system
• CPC Class Codes: Y10S 62/908 Filter or absorber

Abstract

A system for producing cryogenic liquefied industrial gas, especially useful in conjunction with a non-cryogenic industrial gas production facility, wherein the output of the industrial gas production facility is pressurized, a portion passed to the use point, and another portion is condensed against a turboexpanded stream which is also taken from the pressurized gas.

Claims

1. A method for producing cryogenic liquefied industrial gas comprising:

(A) passing industrial gas feed to compression means, compressing the industrial gas feed to produce elevated pressure industrial gas, and passing a first portion of the elevated pressure industrial gas to a use point;

(B) cooling a second portion of the elevated pressure industrial gas to produce cooled industrial gas, and condensing a third portion of the elevated pressure industrial gas to produce cryogenic liquefied industrial gas;

(C) turboexpanding the cooled industrial gas to produce turboexpanded industrial gas, and warming the turboexpanded industrial gas by indirect heat exchange with the second and third portions of the elevated pressure industrial gas to produce warmed turboexpanded industrial gas and said cooled industrial gas and said cryogenic liquefied industrial gas; and

(D) passing the warmed turboexpanded industrial gas to said compression means as part of said industrial gas feed.

2. The method of claim 1 wherein the industrial gas is a fluid comprising from 30 to 99.5 mole percent oxygen.

3. The method of claim 1 wherein the industrial gas is a fluid comprising from 98 to 99.999 mole percent nitrogen.

4. The method of claim 1 wherein at least one of the second portion and the third portion of the elevated pressure industrial gas is increased in pressure prior to the indirect heat exchange with the turboexpanded industrial gas.

5. The method of claim 1 wherein at least one of the second portion and the third portion of the elevated pressure industrial gas is cooled prior to the indirect heat exchange with the turboexpanded industrial gas.

6. Apparatus for producing cryogenic liquefied industrial gas comprising:

(A) compression means for compressing an industrial gas feed to a use pressure;

(B) a heat exchanger, means for passing industrial gas from the compression means to a use point, and means for passing industrial gas from the compression means to the heat exchanger;

(C) a turboexpander, means for withdrawing cryogenic liquefied industrial gas from the heat exchanger, and means for passing industrial gas from the heat exchanger to the turboexpander and from the turboexpander to the heat exchanger; and

(D) means for passing industrial gas from the heat exchanger to the compression means as industrial gas feed.

7. The apparatus of claim 6 further comprising a vacuum pressure swing adsorption industrial gas production facility in flow communication with the compression means.

8. The apparatus of claim 6 further comprising a membrane separation industrial gas production facility in flow communication with the compression means.